Dortmund Data Bank
Azeotropic Data
The experimental data shown in these pages are freely available and have been published already in the DDB Explorer Edition. The data represent a small sub list of all available data in the Dortmund Data Bank. For more data or any further information please search the DDB or contact DDBST.
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 3 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
Search the DDB for all data of this mixture
Data Table
| Azeotropic Type |
T [K] |
P [kPa] |
yaz,1 [mol/mol] |
yaz,2 [mol/mol] |
yaz,3 [mol/mol] |
Measurement Method |
Evaluation |
Source |
| Unspec.Az. |
n.a. |
n.a. |
0.50779 |
n.a.
|
0.29777 |
n.a. |
Author |
2 |
| none |
n.a. |
101.320 |
n.a.
|
n.a.
|
n.a.
|
Phase equilibrium |
Author |
1 |
(yaz - vapor and liquid mole fraction)
List of Azeotrope Types
| Unspec.Az. |
unspecified azeotrope |
| none |
zeotropic |
List of References
| 1 |
Acosta J.; Arce A.; Martinez-Ageitos J.; Rodil E.; Soto A.: Vapor-Liquid Equilibrium of the Ternary System Ethyl Acetate + Hexane + Acetone at 101.32 kPa. J.Chem.Eng.Data 47 (2002) 849-854 |
| 2 |
Bai P.; Zhu L.; Li X.; Zeng J.: Entrainer for Separation of n-Hexane and Ethyl Acetate by Batch Azeotropic Distillation. Shiyou-huagong 35 (2006) 37-41 |
Azeotropic Data Overview
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